STABILIZED PROSTAGLANDIN E>1<

Abstract: A stable and lyophilized formulation of prostaglandin E>1< made by the process comprising a) dissolving PGE-1 in a solution of lactose and tertiary butyl alcohol wherein said tertiary butyl alcohol is present in an amount of from about 15 % to about 33 % volume/volume and the ratio of said lactose to PGE-1 is from about 40,000 to 1 to about 10,000 to 1 weight/weight whereby a formulation of PGE-1 dispersed in lactose is formed; b) adjusting and maintaing the pH of said formulation from about 3.5 to about 6 with an organic acid buffer; c) freezing said formulation to about -50 DEG C; d) drying said formulation to obtain a moisture content of less than 1 % by dry weight and a tertiary butyl alcohol content of less than 3 % by dry weight. Preferably, step c) includes after freezing said formulation to about -50 DEG C, warming to about -25 DEG C for about 2 hours then refreezing to about -50 DEG C. Preferably, the prostaglandin is in an amount of about 25 to 100 ppm in lactose and the pH is maintained at about 4 to 5.

Description: STABILIZED PROSTAGLANDIN E χ Background of the Invention Prostaglandin E 1 (PGE-1) is an inherently unstable compound. PGE-1 is chemically (llα, 13E, 15S)-ll,15-dihydroxy-9-oxoprost-13-en-l-oic acid; or 3-hydroxy- 2-(3-hydroxy-l-octenyl)-5-oxo-cyclopentaneheptanoic acid; and is commonly referred to as alprostadil or PGE^ PGE-1 is a primary prostaglandin which is easily crystallized from purified biological extracts. A goal of this invention was the development of a room temperature stable formulation of PGE-1. More preferred would be a method to stabilize a low dose (5-20 μg) formulation of PGE-1 suitable for use in the treatment of erectile dysfunction. Various attempts to freeze-dry PGE-1 have been described in U.S. Patents 3,952,004 and 3,927,197. The first patent "004 describes the stabilization of PGE-1 in tertiary butyl alcohol and sodium chloride and that lactose or other "simple sugars" destabilize PGE-1. The second patent '197 describes PGE-1 stabilized with tertiary butyl alcohol. Despite various attempts to stabilize PGE-1, better and more effective methods are in demand to increase shelf life and maintain efficacy. PGE-1 formulations in lactose appears to degrade through an apparent second order mechanism with respect to PGE-^ concentration in the solid state. Maximum stability can be achieved by either minimizing the PGE-1 concentration in a suitable lactose diluent or by optimizing other parameters which may impact the second order rate constant. The second order rate constant is affected by the solid state pH, the buffer content, the moisture content, the use of tertiary butyl alcohol during processing, the freezing rate, and the drying rate. All of these parameters have been optimized to minimize the value of the second order rate constant. Summary of the Invention In one aspect the subject invention is a lyophilized formulation of PGE-1 made by the process comprising: a) dissolving PGE-1 in a solution of lactose and tertiary butyl alcohol wherein the tertiary butyl alcohol is present in an amount of from about 15% to 33% volume/volume and the ratio of lactose to PGE-1 is from about 40,000 to 1 to about 10,000 to 1 weight/weight (25 to 100 ppm in lactose) whereby a formulation of PGE- ldispersed in lactose is formed; b) adjusting and maintaining the pH of the formulation from about 3.5 to about 6 with an organic acid buffer (preferably sodium citrate); c) freezing the formulation to about -50°C; and d) drying the formulation to obtain a moisture content of less than 1% by dry weight and a tertiary butyl alcohol content of less than 3% by dry weight. Preferably, the PGE-1 in the formulation is in an amount of about 25 to 100 ppm lactose and the pH is adjusted and maintained at 4 to 5 by the presence of a buffer. Preferably, the freezing step (c) includes an annealing process by freezing the formulation to about -50°C, warming to about -25°C for about 2 hours then refreezing to about -50°C. In another aspect, the subject invention is a method for preparing a stabilized, lyophilized formulation of PGE-1 comprising the steps set forth above. In yet another aspect, the present invention is a freeze-dried formulation of PGE-1 for use in the treatment of erectile dysfunction. Typical dosages of the formulation are (5-20 μg) formulations of PGE-1. These formulations correspond to a ratio of lactose to PGE-1 of from about 40,000 to 1 to about 10,000 to 1 weight/weight (25 to 100 ppm in lactose). That is, 5 μg corresponds to 40,000 to 1; 10 μg corresponds to 20,000 to 1 and 20 μg corresponds to 10,000 to 1. Detailed Description of the Invention The subject invention is a lyophilized PGE-1 composition made from a bulk sterile filtered solution which contains 20% v/v tertiary butyl alcohol (TBA) and has an apparent pH of approximately 4. Both the water and TBA are removed during the freeze-drying process. Residual water and TBA remaining after lyophilization are < 0.5% and 0.5-2% respectively of the dried cake mass. In one formulation, a vial dosage contains after completion of lyophilization: 23 μg of PGE-1 (alprostadil), 193.8 mg of anhydrous lactose, and 53 μg of sodium citrate. After reconstitution of this freeze-dried powder with 1.0 ml of either water for injection or bacteriostatic water for injection, a solution containing 20 ug/ml of PGE-1 is obtained. The freeze- dried powder is packaged in a 5 ml vial and sealed with a lyophilization style closure within the freeze-dry chamber, and capped with an aluminum overseal. The chemical stability of the PGE-1 can be predicted by use of the Arrhenius equation and accelerated stability data. Initial rate kinetic analyses (i.e., monitoring the rate of formation of the major degradation product, PGA-^) can be used to assess the chemical stability. The projected stability analysis indicates that when the product is properly manufactured with the optimized formulation and process, the shelf-life should be greater than 24 months when the product is stored at 25°C or less. Initial work centered on the use of a lactose diluent and lyophilization from a tertiary butyl alcohol (TBAVwater co-solvent system. The freeze-dried formulation produced appeared to possess the properties of a solid solution. The degradation of the PGE-1 in this type of formulation could be best described by a second order mechanism. Stability could be increased by maximizing the amount of lactose diluent or minimizing the amount of PGE-1 present. The solid state second order kinetics fit well to an Arrhenius type temperature relationship. Residual moisture was shown to have a deleterious effect on the stability. The pH of the cake also affected the stabiUty. Optimum stability was achieved at about pH 4-5. A minimum amount of citrate buffer was added to the formula to control pH. Lyophilization from a TBA/water co-solvent mixture improved stability of the formulations compared to water only. Typically, standard freeze drying techniques can be used to prepare the stabilized PGE-1. More preferably, an annealing technique can be performed to decrease and more uniformly control the residual tertiary butyl alcohol in the freeze dried product. Optimum stability was achieved when freeze-drying from a 17-25% TBA/water mixture. The method for preparing a stabilized, freeze-dried formulation of PGE-1 controls key parameters which affect product stability including the following: the level of lactose diluent present, the apparent pH of the lyophilized cake, the moisture content, the use of the co-solvent tertiary butyl alcohol during processing, the freezing rate and methodology prior to lyophilization, the freeze-drying rate, and the size of the vial used to manufacture the product. Lyophilization of a buffered lactose formulation of PGE-1 from a tertiary butyl alcohol (TBA) / water mixture provides superior product stability than when freeze-drying from only an aqueous system. The level of TBA which afforded the product maximum stabiUty appeared to be when the TBA amount ranged from 17- 25% (v/v). The 20% TBA level was selected as the amount of co-solvent for the PGE- 1 formulation since it feU within the optimum co-solvent range. The lower the level of TBA used also reduced the flammabiUty potential, reduced the amount of TBA waste which would be generated after lyophiUzation, reduced the level of isopropyl alcohol (a process impurity in the TBA) in the product, and lowered the precipitation potential during manufacturing for the lactose from the co-solvent system. Stability data clearly indicated that lyophilization of the buffered lactose formulation of PGE- 1 from a TBA/water co-solvent system would be significantly more stable than freeze-drying from an aqueous system. The mechanism for the improvement in stabiUty when using the TBA is unknown but it is likely enabUng the PGE-1 molecules to be kept further apart during the freezing and lyophiUzation phases of manufacture. Therefore, it is recommended that the final formulation be lyophiUzed from a co-solvent system containing 20% v/v TBA. It is important that this level of TBA be used because lower levels of TBA (< 17%) in the final formulation will produce a product which is much less stable than when using at least 20% TBA. The resulting residual TBA in the final product is expected to be approximately 0.5 to 2% of the cake weight. A safety assessment of TBA and its impurities (isopropyl alcohol, 2-butyl alcohol, and isobutyl alcohol) concluded that TBA levels of not more than 3% of a 200 mg freeze-dried cake was acceptable and that other residual organic solvents should be not more than 0.5% of a 200 mg freeze-dried cake. The appUcation of heat to the lactose may adversely affect product stability. The stabiUty data clearly dictates that close control of the freeze-dry cycle (both primary and secondary drying) is critical to reproducible manufacture lots with equivalent stabiUty. Stability can therefore be a function of processing parameters. Since the PGE-1 degradation kinetics fit (at least empiricaUy) a second order mechanism, stabiUty can be improved by simple dilution of the PGE-1 with lactose. This would suggest that maximizing the amount of lactose for a given amount of PGE-1 should provide the optimum stability. For a 20 μg/ml formulation of PGE-1 the amount of lactose chosen for formulating the optimum formulation is 204 mg of lactose monohydrate. After lyophilization, the 5% water is removed and the resulting lactose present in the vial is 193.8 mg. The cake volume for 193.8 mg of anhydrous lactose is approximately 0.13 ml. Therefore, the theoretical solution concentration of lactose after reconstitution with 1.0 ml is (193.8 mg/1.13 ml) or 172 mg/ml. The amount of PGE-1 needed to produce a 20 μg/ml solution after reconstitution with 1.0 ml is (1.13 ml X 20 μg/ml) or 22.6 μg. It has been determined that the cake pH also affected product stability. Maximum stabiUty is achieved when the cake pH is held near pH 4 to 5. Both citrate and acetate buffers can be used; however, citrate buffer was selected as the buffer of choice for the PGE-1 formula since it is a common buffer for parenteral products. Since PGE-1 is susceptible to both acid and base hydrolysis, it is probable that some buffer catalysis of the PGE-1 molecule may occur. The amount of citrate buffer selected for the final formulation was chosen based on a compromise between sufficient buffer to adequately control pH and yet not itself significantly provide an alternate catalytic route. The level of citrate chosen for the final formulation was 53 μg of sodium citrate / 23 μg PGE-1 (3.17 moles citrate / mole PGE-1). This level of citrate will theoretically cause only a relatively minor increase (< 7%) in the degradation rate constant. In order to determine if sufficient buffer was present to control pH for the shelf Ufe of the product, samples with this amount of buffer present were degraded to less than 90% of initial potency under accelerated conditions. The pH was measured initially and after the > 10% drop in potency had taken place. No significant change in pH occurred. This demonstrates that sufficient buffer was present to maintain pH during the normal shelf life of the product where less than 10% degradation will take place. The presence of moisture in the product will have a negative impact on product stabiUty. It is therefore preferred that the formulation have the level of moisture as low as possible during the processing and to maintain that level throughout the shelf life of the product. The rate of freezing also has an effect on product stabiUty. The unique kinetics of the degradation pathway indicates that it is imperative that the PGE-1 molecules be kept as far apart as possible in order to minimize the interaction of two PGE-1 molecules. Typically, the lyophiUzation cycle is designed to proceed as fast as possible without exceeding the melting temperature of the frozen solution during primary drying. Therefore, as long as no meltback occurs during the primary drying phase and the water content is reduced to a sufficiently low level during the secondary drying phase, then the product would normally be acceptable. However, the PGE-1 formulation can be quite different from the normal situation because the major component in the formulation is lactose. The Uterature reports that lactose possesses a very low glass transition temperature (T ) which is on the order of - 31°C. It is possible to lyophiUze above the glass transition temperature for an excipient such as lactose without exceeding the melting temperature of the bulk solution. If the product temperature exceeds T , the frozen solution viscosity decreases significantly resulting in a rubbery system where the mobiUty of the PGE- 1 molecules will increase substantiaUy. This type of event could lead to a situation where the PGE-1 molecules could either aggregate, miceUize, or come into closer proximity than if the frozen solution is kept below the T . It is important, therefore, that the drying cycle be optimized to prevent such an occurrence from happening. Typically, the PGE-1 in lactose formulation is freeze dried using standard techniques, More preferred, an annealing process is used to enable the residual tertiary butyl alcohol to be reduced and controUed. In an annealing process the initial stage of the freeze drying process is carried out by freezing the PGE-1 formulation to about -50°C, warming it to about -25°C for about 2 hours then refreezing it to about -50°C. Next, the freeze drying is continued to obtain a moisture content of less than 1% by dry weight and a tertiary butyl alcohol content of less than 3% by dry weight. The conclusion is that in order to achieve the proper product stabiUty, not only must the formulation be carefuUy chosen, but also the manufacturing process must be appropriately optimized. The mechanisms may not be fuUy understood on a theoretical basis at this time, however, the effects described are reproducible. It is therefore, mandated that a conservative cycle be used to consistently achieve maximum product stabiUty. Prototype lactose base formulations of PGE-1 indicated that the stabiUty correlated weU with an Arrhenius type temperature relationship. This fit to an Arrhenius relationship was apparent whether the rate constants were plotted for the degradation rate of PGE-1 or for the rate of formation of the major degradation product PGA- j^ . Therefore, the stabiUty of the lactose formulation for PGE-1 can be accurately assessed by initial rate type kinetic analysis (i.e., by monitoring the rate of PGA-^ formation). Optimization of a freeze-dried formulation PGE-1 (Alprostadil S.Po.) and preferably as designed for use in an injectable such as in the treatment of erectile dysfunction has been determined as explained above. The formulation appears to degrade through an apparent second order mechanism with respect to PGE-1 concentration in the soUd state. Maximum stability can be achieved by either minimizing the PGE-1 concentration in the lactose diluent or by optimizing those parameters which impact the second order rate constant. The amount of lactose diluent chosen for the optimized formulation was based on solubility Umitations and the irritation potential of the lactose. In one embodiment the amount of PGE-1 present was based on the proposed cUnical dose for an injection volume of 1 ml or less. The second order rate constant is affected by the soUd state pH, the buffer content, the moisture content, the use of tertiary butyl alcohol during processing, the freezing rate, and the drying rate. AU of these have been optimized to minimize the value of the second order rate constant. The product is lyophilized from a bulk sterile filtered solution which contains 20% v/v tertiary butyl alcohol (TBA) and has an apparent pH of approximately 4. Both the water and TBA are removed during the freeze-drying process. Residual water and TBA remaining after lyophiUzation are < 0.5% and 0.5 to 2% respectively of the dried cake mass. The final formulation, for example, per vial contains after completion of lyophiUzation: 23 μg of PGE-1 (alprostadil), 193.8 mg of anhydrous lactose, and 53 μg of sodium citrate. After reconstitution of this freeze-dried powder with 1.0 ml of either water for injection or bacteriostatic water for injection, a solution containing 20 μg/ml of PGE-1 will be obtained. Or, the final formulation, for example, per vial contains after completion of lyophiUzation: 11.9 μg of PGE-1 (alprostadil), 193.8 mg of anhydrous lactose, and 53 μg of sodium citrate. After reconstitution of this freeze-dried powder with 1.0 ml of either water for injection or bacteriostatic water for injection, a solution containing 10 μg/ml of PGE-1 wiU be obtained. Or, the final formulation, for example, per vial contains after completion of lyophiUzation: 6.1 μg of PGE-1 (alprostadil), 193.8 mg of anhydrous lactose, and 53 μg of sodium citrate. After reconstitution of this freeze-dried powder with 1.0 ml of either water for injection or bacteriostatic water for injection, a solution containing 5 μg/ml of PGE-1 wiU be obtained. The freeze-dried powder, as per these examples, is packaged in a 5 ml vial, sealed with a lyophiUzation style closure within the freeze-dry chamber, and capped with an aluminum overseal. The chemical stabiUty of the PGE-1 can be predicted by use of the Arrhenius equation and accelerated stability data. Initial rate kinetic analyses (i.e., monitoring the rate of formation of the major degradation product, PGA-^) can also be used to assess the chemical stabiUty. The projected stabiUty analysis indicates that when the product is properly manufactured with the optimized formulation and process, the shelf-life should be greater than 24 months when the product is stored at 25°C or less. A lot for the various strengths of PGE-1 stabilized product freeze dried under the conditions described above was prepared and stability measured. The results are shown in the Tables that foUow: TABLE I. 20 μg Strength Time (months) Potency at 5°C Potency at 25°C (% of Initial) (% of Initial) 0 100.5% 100.5% 0 100.0% 100.0% 0 100.5% 100.5% 0 99.5% 99.5% 0 100.0% 100.0% 3 99.5% 100.5% 3 100.5% 101.5% 6 100.0% 98.5% 6 100.5% 9 99.5% 96.6% 9 99.0% 98.5% 11.44 100.0% 96.6% 11.44 99.5% 96.6% 11.44 99.5% 96.1% 12 99.5% 97.6% 12 100.5% 97.6% 12 101.0% 97.6% 12 101.0% 97.6% 15 101.0% 96.1% 15 102.0% 95.6% • 18 100.0% 95.6% 18 99.5% 94.6% 21 99.0% 96.1% 21 99.5% 95.1% TABLE II. 10 μg Strength Time (months) Potency at 5°C Potency at 25°C (% of Initial) (% of Initial) 0 99.1% 99.1% 0 100.9% 100.9% 0 100.0% 100.0% 0 100.0% 100.0% 0 99.1% 99.1% 0 101.9% 101.9% 0 100.9% 100.9% 0 100.9% 100.9% 0 100.0% 100.0% 0 100.0% 100.0% 1 99.1% 102.8% 1 100.0% 102.8% 1 100.0% 102.8% 2 100.9% 102.8% 2 102.8% 102.8% 2 102.8% 102.8% 3 99.1% 100.0% 3 100.9% 99.1% 3 99.1% 98.1% 4 100.9% 100.9% 4 100.9% 100.9% 4 100.9% 100.0% 5 100.0% 97.2% 5 100.0% 99.1% 5 100.0% 99.1% 6 98.1% 97.2% 6 97.2% 98.1% 6 96.3% 98.1% 7.95 97.2% — 7.95 98.1% — Time (months) Potency at 5°C Potency at 25°C (% of Initial) (% of Initial) 7.99 98.1% — 7.99 98.1% — 8 98.1% — 8 97.2% — 9 101.9% 99.1% 9 100.9% 99.1% 9 102.8% 100.0% 12 98.1% 97.2% 12 98.1% 96.3% 12 99.1% 96.3% 15 99.1% 96.3% 15 99.1% 94.3% 15 99.1% 95.3% TABLE III. 5 μg Strength Time (months) Potency at 5°C Potency at 25°C (% of Initial) (% of Initial) 0 101.5% 101.5% 0 99.3% 99.3% 0 100.4% 100.4% 0 98.9% 98.9% 0 99.6% 99.6% 0 99.8% 99.8% 0 99.6% 99.6% 0 100.9% 100.9% 0 100.2% 100.2% 0 100.4% 100.4% 1 101.1% 100.7% 1 100.7% 99.4% 1 100.2% 99.8% 2 100.0% 99.3% 2 100.6% 100.7% 2 100.6% 99.4% 3 100.4% 99.8% 3 100.4% 100.2% 3 100.6% 99.8% 4 103.5% 100.0% 4 99.6% 99.4% 4 100.6% 100.6% 5 98.9% 99.4% 5 100.0% 99.4% 5 100.9% 100.2% 6 100.7% 99.4% 6 100.9% 99.6% 6 100.9% 100.2% Time (months) Potency at 5°C Potency at 25°C (% of Initial) (% of Initial) 6 100.0% 99.1% 6 99.3% 98.5%) The Tables show that exceUent stability was maintained for the Ufe of lyophiUzed product.

Claims: What is Claimed: 1. A lyophiUzed formulation of PGE-1 made by the process comprising: a) dissolving PGE-1 in a solution of lactose and tertiary butyl alcohol wherein said tertiary butyl alcohol is present in an amount of from about 15% to about 33% volume/volume and the ratio of said lactose to PGE-1 is from about 40,000 to 1 to about 10,000 to 1 weight/weight whereby a formulation of PGE-1 dispersed in lactose is formed; b) adjusting and maintaining the pH of said formulation from about 3.5 to about 6 with an organic acid buffer; c) freezing said formulation to about -50°C; and d) drying said formulation to obtain a moisture content of less than 1% by dry weight and a tertiary butyl alcohol content of less than 3% by dry weight. 2. The lyophUized formulation of PGE-1 made by the process of Claim 1 wherein said step c) includes after freezing said formulation to about -50°C, warming to about -25°C for about 2 hours then refreezing to about -50°C. 3. The lyophiUzed formulation of PGE-1 made by the process of Claim 1 wherein in said organic acid buffer of step b) is sodium citrate. 4. The lyophiUzed formulation of PGE-1 made by the process of Claim 1 wherein in PGE-1 is in an amount of about 25 to about 100 ppm in lactose. 5. The lyophilized formulation of PGE-1 made by the process of Claim 1 wherein step b) is adjusting and maintaining the pH of said formulation from 4 to 5 with an organic acid buffer. 6. A method for preparing a stabihzed, lyophilized formulation of PGE-1 comprising the steps of: a) dissolving PGE-1 in a solution of lactose and tertiary butyl alcohol wherein said tertiary butyl alcohol is present in an amount of from about 15% to about 33% volume/volume and the ratio of said lactose to PGE-1 is from about 40,000 to 1 to about 10,000 to 1 weight/weight whereby a formulation of PGE- ldispersed in lactose is formed; b) adjusting and maintaining the pH of said formulation from about 3.5 to about 6 with an organic acid buffer; c) freezing said formulation to about -50°C; and d) drying said formulation to obtain a moisture content of less than 1% by dry weight and a tertiary butyl alcohol content of less than 3% by dry weight. 7. The method of Claim 6 wherein said step c) includes after freezing said formulation to about -50°C, warming to about -25°C for about 2 hours then refreezing to about -50°C. 8. The method of Claim 6 wherein in said organic acid buffer of step b) is sodium citrate. 9. The method of Claim 6 wherein in PGE-1 is in an amount of about 25 to about 100 ppm in lactose. 10. The method of Claim 6 wherein step b) is adjusting and maintaining the pH of said formulation from 4 to 5 with an organic acid buffer.

Inventors: GOLD PAUL M, PETRE WILLIAM J, TEAGARDEN DIRK L, GOLD, PAUL, M., PETRE, WILLIAM, J., TEAGARDEN, DIRK, L.
Applicants: GOLD PAUL M, PETRE WILLIAM J, TEAGARDEN DIRK L, UPJOHN CO, GOLD, PAUL, M., PETRE, WILLIAM, J., TEAGARDEN, DIRK, L., THE UPJOHN COMPANY
Application year: 1994
Main classification: A61K31
IPC codes: A61K9, A61K31, A61K47